Integrated unit for intake and pretreatment with local backwashing

ABSTRACT

A local backwashing apparatus  110  for a filtering system comprises an enclosure  119  having an open lower end, positionable above a surface of filter media  92  supported by a drainage layer  96.  The enclosure is connected to a mechanical member ( 300,  FIG.  6 A) configured to force the enclosure into the filter media and release the force prior to the lower end of the enclosure contacting the drainage layer. The lower end of the enclosure being brought into contact with the drainage layer through a pressure differential between the interior and exterior of the enclosure. A pneumatic system such as an air pump, is in fluid communication with the upper part  127  of the enclosure and is configured to determine an air pressure therein. A pipe system connects the upper part of the enclosure with the pneumatic system and with a discharge structure  132.  A control unit is connected to the pneumatic system. Also disclosed is a method of backwashing a filtering system. The backwashing apparatus may be used to pre-treat water.

This application is a continuation of U.S. application Ser. No.16/093,924 filed Oct. 15, 2018, which claims priority to 1613443.9 filedApr. 14, 2016, which are hereby incorporated by reference in theirentirety.

TECHNICAL FIELD

The present invention relates to the field of water treatment, and moreparticularly, to a filtering system.

BACKGROUND

Water treatment systems such as seawater desalination facilities andosmotic power plants (facilities that generate energy from a differencein osmotic pressures of e.g. seawater versus river water) include anintake unit for delivering water from its source (e.g. sea or river) tothe system, and a pretreatment unit for removing floating and dissolvedmaterial from the delivered water, in order to prepare the water for themain membrane process.

Two types of intake units are open intakes and infiltration intakes (orinfiltration galleries). Open intakes draw water via piping directlyfrom the source. Open intakes typically employ screen meshes to filterout large debris and prevent fish or other marine life from being drawninto the pumps. However, millions of fish and other small marineorganisms, with a width of under 2 cm are sucked into the piping,leading to considerable damage, both to the environment and tofacilities. Damage is inflicted on both large aquatic organisms such asfish or crabs that are trapped against the intake screens and drown orsuffocate, and on small marine organisms such as fish, fish eggs, larvaeor plankton that is drawn into the intake system and is killed by theplant equipment.

Infiltration intakes, or galleries, are built in the seabed by theinstallation of horizontal drain systems. The drain system is placed inthe natural filtration media sand, and the seawater is slowly filteredby the sand. This media is naturally cleaned by waves and storms.Horizontal drain systems deliver water to the pumping station located onthe seashore. Infiltration galleries, while protecting the marineenvironment, can only be installed in areas with naturally occurringsands. Another major limitation is that these systems clog over time andit is highly difficult, or in some cases impossible, to clean them.Clogged media reduces the throughput through the system by two orders ofmagnitude (e.g. from 10 to 0.1 m3/hr).

Pretreatment units employ a layer of filter media supported by adrainage layer. Water is introduced above the filter media, and ispretreated by flowing through the filter media which removes floatingand dissolved material therefrom. The filter media is gradually cloggedby the removed material, and periodical global backwashing is used toclean the filter media. Global back washing produces huge amounts ofwastewater which leads to environmental and technical problems. Thebackwashing process also involves interrupting the operation of thefilter, and this is a major drawback too.

Such a global backwashing system according to the prior art isillustrated in FIG. 1A. FIG. 1A illustrates a prior art filter cleaningmethod for back washing a filter 90 that is used to filter water 91through filter media 92 into a drainage layer 96 (under-drain) thatsupports filter media 92. The filter cleaning method uses an externalsource of backwash water that is pumped throughout the whole filter 90to backwash the filter globally (see arrows). The backwash water is thenremoved gravitationally through a discharge channel 132. The largevolume of backwash water requires operation of the filter with a highlevel of water 91 above filter media 92 (denoted in FIG. 1A by H) toallow for expansion of the filter media, during which sludge is releasedfrom the filter media particles. The necessarily large water head hassevere constructional implications, as the substrate must support thelarge pressures. Hence, prior art backwashing systems suffer from asevere limitation. Clearly, this method of backwashing is not applicableto infiltration intakes as they are open to the water source (such as asea or a river) and contamination of the source with the backwash wateris hardly acceptable.

U.S. Pat. No. 4,486,307 (Weiler) describes a filter apparatus havingfilter bed back-washing means comprising a raisable and lowerablesuction bell, the side walls of which define division walls to compartthe respective partial volume of the filter bed to be cleaned. Thesuction bell is mounted on a bridge and the bell is raised and loweredby a lifting device. The bell is connected to a suction pump mounted onthe bridge. In order to clean the filter bed of suspended matterfiltered out of the crude water to be purified, the suction bell islowered into an operative position. In order to facilitate thepenetration of the lower edges of the side walls of the bell, the wallsare provided with sharp stabbing edges and a vibrator is arranged on thetop side of the suction bell. The suction action sucks water out of thefiltrate chamber to make the bottom permeable to liquids. As the partialvolume of the filter bed located in the suction bell is washed, the sandof the filter bed is loosened and eddied whereby the suspended matterretained in the respective partial volume is loosened and exhausted bythe suction action of the pump.

U.S. Pat. No. 4,988,439 (Medders) relates to liquid filtration systemshaving a travelling bridge-type cleaning apparatus for sequentiallycleaning a plurality of suspended solids filter units. The carriagemeans carries a hood assembly enclosing air scour means and liquidbackwash means, the hood assembly being provided with sealing means toestablish a substantially air and wafer tight seal between the hood anda filter cell.

While these systems are satisfactory, backwashing of a sand bed used asthe filter media suffers for the severe drawback of obtaining sufficientpenetration of the compacted sand bed to obtain adequate filtering ofthe water through the filter media.

It is an object of the present invention to provide an improved methodand apparatus for backwashing a filtering system that aims to overcome,or at least alleviate, the abovementioned drawbacks.

BRIEF SUMMARY

A first aspect of the present invention provides a local backwashingapparatus for a filtering system comprising:

-   -   an enclosure having an open lower end for positioning above a        surface of filter medial of the filtering system, the filter        media supported by a drainage layer;    -   a pneumatic system in fluid communication with an upper part of        the enclosure and configured to determine an air pressure in an        upper past;    -   a pipe system connecting the upper pan of the enclosure with the        pneumatic system and with a discharge structure; and    -   a control unit connected to the pneumatic system and configured        to conduct local backwashing of consecutive partial volumes of        the filter media by sinking the enclosure into the filter media        until the enclosure is supported on the drainage layer by        reducing the air pressure in the upper part of the enclosure        through the pneumatic system once the open lower end of the        enclosure is immersed in filter media, to enclose the partial        volume of filter media within the enclosure and generating local        backwashing of the partial volume of the filter media enclosed        in the enclosure, during continued operation of global filtering        through filter media outside the enclosure in the filtering        system, by generating suction through the pneumatic system that        initiates a water flow from the upper part of the enclosure        through the pipe system to the discharge structure, wherein the        water flow introduces into the lower end of the enclosed partial        volume of filter media filtered water from the drainage layer        which expands the enclosed filter media and releases sludge        therefrom the water flow that flows to the discharge structure;        and raising the enclosure above the surface of the filter media        to release the backwashed volume of filter media, by injecting        air and increasing the air pressure in the upper part of the        enclosure through the pneumatic system to float the enclosure        above the filter media;    -   characterized in that the enclosure comprises side walls with a        roof, the free ends of the side walls forming the open lower end        of the enclosure, the free ends converging to provide an open        lower end with a smaller cross-sectional area than the upper        part of the enclosure.

According to a second aspect of the present invention there is providesa local backwashing apparatus for a filtering system comprising:

-   -   an enclosure having an open lower end for positioning above a        surface of filter medial of the filtering system, the filter        media supported by a drainage layer;    -   a pneumatic system in fluid communication with an upper part of        the enclosure and configured to determine an air pressure in an        upper part;    -   a pipe system connecting the upper part of the enclosure with        the pneumatic system and with a discharge structure; and    -   a control unit connected to the pneumatic system and configured        to conduct local backwashing of consecutive partial volumes of        the filter media by sinking the enclosure into the filter media        until the enclosure is supported on the drainage layer by        reducing the air pressure in the upper part of the enclosure        through the pneumatic system once the open lower end of the        enclosure is immersed in filter media, to enclose the partial        volume of filter media within the enclosure and generating local        backwashing of the partial volume of the filter media enclosed        in the enclosure, during continued operation of global filtering        through filter media outside the enclosure in the filtering        system, by generating suction through the pneumatic system that        initiates a water flow from the upper part of the enclosure        through the pipe system to the discharge structure, wherein the        water flow introduces into the lower end of the enclosed partial        volume of filter media filtered water from the drainage layer        which expands the enclosed filter media and releases sludge        therefrom the water flow that flows to the discharge structure;        and raising the enclosure above the surface of the filter media        to release the backwashed volume of filter media, by injecting        air and increasing the air pressure in the upper part of the        enclosure through the pneumatic system to float the enclosure        above the filter media;    -   characterized in that the enclosure is provided with a water        inlet for selective delivery of water from outside the enclosure        to within the enclosure during sinking of the enclosure into the        filter media.

Preferably, the water inlet is provided with a valve which allows acontrolled amount of water to enter the enclosure during sinking of theenclosure, into the filter media. More preferably, the water inlet isgradually closed as suction is generated by the pneumatic system toinitiate water flow through the enclosure from the filter media.

According to a third aspect of the present invention there is provides alocal backwashing apparatus for a filtering system comprising:

-   -   an enclosure having an open lower end for positioning above a        surface of filter medial of the filtering system, the filter        media supported by a drainage layer,    -   a pneumatic system in fluid communication with an upper part of        the enclosure and configured to determine an air pressure in an        upper part;    -   a pipe system connecting the upper part of the enclosure with        the pneumatic system and with a discharge structure; and    -   a control unit connected to the pneumatic system and configured        to conduct local backwashing of consecutive partial volumes of        the filter media by sinking the enclosure into the filter media        until the enclosure is supported on the drainage layer by        reducing the air pressure in the upper part of the enclosure        through the pneumatic system once the open lower end of the        enclosure is immersed in filter media, to enclose the partial        volume of filter media within the enclosure and generating local        backwashing of the partial volume of the filter media enclosed        in the enclosure, during continued operation of global filtering        through filter media outside the enclosure in the filtering        system, by generating suction through the pneumatic system that        initiates a water flow from the upper part of the enclosure        through the pipe system to the discharge structure, wherein the        water flow introduces into the lower end of the enclosed partial        volume of filter media filtered water from the drainage layer        which expands the enclosed filter media and releases sludge        therefrom the water flow that flows to the discharge structure;        and raising the enclosure above the surface of the filter media        to release the backwashed volume of filter media, by injecting        air and increasing the air pressure in the upper part of the        enclosure through the pneumatic system to float the enclosure        above the filter media;    -   characterized in that the enclosure is connected to a mechanical        member configured to forcibly drive the enclosure into the        filter media and release said force prior to contact of the        lower end of the enclosure with the drainage layer, the lower        end of the enclosure being brought into contact with the        drainage layer through a pressure differential between the        interior and exterior of the enclosure.

Any appropriate mechanical member may forcibly drive the enclosurethrough the filter media, such as a piston. The mechanical memberpreferably drives the enclosure through 95-99% of the filter media priorto its release, A distance of 1-10 cm is preferably provided between thelower end of the enclosure and the drainage layer for movement of theenclosure by means of the pressure differential.

It is to be appreciated that the apparatus of the present inventionpreferably includes the features of the first, second and third aspectsof the present invention.

The apparatus preferably includes a supporting structure movablysupporting the enclosure, the supporting structure configured toposition the enclosure at specified spots on the surface of the filtermedia. The supporting structure may be at least one a fixed bridge, afloating bridge, a rotating bridge or a crane.

The open lower end of the enclosure preferably has an area between 0.5m³ and 1.5 m², preferably with the main body of the enclosure being atleast 10% greater than this area, preferably more than 25%.

The filtering system maybe elongated with the enclosure spanning a widthof the filtering system.

The control unit is preferably arranged to sequentially backwash a wholevolume of the filter media at a frequency of between five times a dayand once in three months.

Preferably, a height of the enclosure is larger than a height of thewater above the filter media in respect to the drainage layer.

A further aspect of the present invention provides a method ofbackwashing a filtering system having a layer of filter media supportedby a drainage layer. The method comprises: sequentially backwashingpartial volumes of the filter media by (i) driving the enclosure intothe filter media until the enclosure is above the drainage layer bymechanical forcing the enclosure through the media (ii) reducing the airpressure in an upper part of the enclosure once the open lower end ofthe enclosure is immersed in filter media, to enclose the partial volumeof filter media within the enclosure, (iii) allowing the enclosure tocome into contact with the drainage layer by a pressure differentialbetween an interior and exterior of the enclosure (iv) generating localbackwashing of the partial volume of the filter media enclosed in theenclosure, during continued operation of global filtering through filtermedia outside the enclosure in the filtering system, by generatingsuction in the upper part of the enclosure that initiates a water flowfrom the upper part of the enclosure through the pipe system to thedischarge structure, wherein the water flow introduces into the lowerend of the enclosed partial volume of filter media filtered water fromthe drainage layer which expands the enclosed filter media and releasessludge therefrom to the water flow, and (v) raising the enclosure abovethe surface of the filter media to release the backwashed enclosedvolume of filter media, by injecting air and increasing air pressure inthe upper part of the enclosure to float the enclosure above the filtermedia.

Alternatively, or additionally, the method may comprise (i) sinking theenclosure into the filter media whilst simultaneously delivering waterinto the enclosure (ii) reducing the air pressure in an upper part ofthe enclosure once the open lower end of the enclosure is immersed infilter media, to enclose the partial volume of filter media within theenclosure, (iii) reducing and then ceasing delivering water into theenclosure (iv) generating local backwashing of the partial volume of thefilter media enclosed in the enclosure, during continued operation ofglobal filtering through filter media outside the enclosure in thefiltering system, by generating suction in the upper part of theenclosure that initiates a water flow from the upper part of theenclosure through the pipe system to the discharge structure, whereinthe water flow introduces into the lower end of the enclosed partialvolume of filter media filtered water from the drainage layer whichexpands the enclosed filter media and releases sludge therefrom to thewater flow, and (v) raising the enclosure above the surface of thefilter media to release the backwashed enclosed volume of filter media,by injecting air and increasing air pressure in the upper part of theenclosure to float the enclosure above the filter media.

BRIEF DESCRIPTION OF THE DRAWINGS

For a better understanding of embodiments of the invention and to showhow the same may be carried into effect, reference will now be made,purely by way of example, to the accompanying drawings in which likenumerals designate corresponding elements or sections throughout.

In the accompanying drawings:

FIGS. 1A and 1B illustrate schematically global and local backwashingapparatus and methods, respectively, in respect to the prior art;

FIG. 2 is a schematic block diagram illustrating an integrated intakeand pretreatment unit for a water treatment plant;

FIGS. 3A-3E schematically illustrate the operation of the localbackwashing apparatus within a filtering system, according to someembodiments of the invention;

FIGS. 4A-4C schematically illustrate integrated intake and pretreatmentunits for a water treatment plant with various configurations of thesupporting structure for the local backwashing apparatus;

FIG. 5 is a schematic flowchart illustrating a method of supplying awater treatment plant with water and backwashing of the filteringsystem, according to some embodiments of the invention; and

FIGS. 6A and 6B are schematic diagrams illustrating a two-step processfor insertion of an enclosure into a filter media, according to oneembodiment of the present invention;

DETAILED DESCRIPTION

With specific reference now to the drawings in detail, it is stressedthat the particulars shown are by way of example and for purposes ofillustrative discussion of the preferred embodiments of the presentinvention only, and are presented in the cause of providing what isbelieved to be the most useful and readily understood description of theprinciples and conceptual aspects of the invention. In this regard, noattempt is made to show structural details of the invention in moredetail than is necessary for a fundamental understanding of theinvention, the description taken with the drawings making apparent tothose skilled in the art how the several forms of the invention may beembodied in practice.

Before explaining at least one embodiment of the invention in detail, itis to be understood that the invention is not limited in its applicationto the details of construction and the arrangement of the components setforth in the following description or illustrated in the drawings. Theinvention is applicable to other embodiments or of being practiced orcarried out in various ways and is limited only by the appended claims.Also, it is to be understood that the phraseology and terminologyemployed herein is for the purpose of description and should not beregarded as limiting.

The following illustrates a filtering system and an apparatus forperforming local or spot backwashing of a water treatment unit(including also water intake units and water pretreatment units) thatfilters water using a layer of filter media (e.g. sand filter usingsand). The apparatus is moved above the surface of the filter media andis inserted at different parts of it consecutively, to eventuallybackwash the whole volume of the filter media.

The apparatus comprises an enclosure (that may be supported on a bridge,a tower, a crane or a floating platform) that is sunk into the filtermedia and encloses a portion of it. The enclosure is supported on thedraining structure at the base of the filter media. Sinking theenclosure is carried out by lowering the air pressure in its upper part.

Once sunk into the filter media, the lowered air pressure in the upperpan of the enclosure is used to initiate suction in the enclosure thatexpands the enclosed portion of filter media and removes water withsludge from it. The water is supplied into the enclosure from filteredwater entering the enclosure from the surrounding filter media outsidethe enclosure, as the filtration continues globally in the wafertreatment unit (through filter media outside the enclosure in thefiltering system). The enclosure allows a local rise in the water levelthat does not produce a large head when viewed on the scale of the wholesystem, and hence does not require massive structural adaptations.Indeed, using local backwashing allows the water level above the filtermedia to be low, simplifying the construction of the whole system.

After water with sludge is removed, the enclosed portion of filter mediais allowed to settle, and the enclosure is raised out of the filtermedia by increasing the air pressure in its upper part. Upon thisincrease, the enclosure floats and is moved to another area of thefilter.

Several benefits are achieved by using this type of localisedbackwashing system. The design of the water treatment plant issimplified by using a single filter system which integrates the intakeand pretreatment functions instead of having two separate units. Thefiltering unit has a better design than prior art pretreatment units dueto the lower water head that is made possible by the local backwashingapparatus and method and the backwashing process is more efficient,using a much smaller quantity of water, avoiding the use of largeexternal reservoirs of both backwash water and sludge holdingwastewater, and allowing the continued operation of the filtering systemduring the local backwashing. Furthermore, intake of water from thesource is made possible without damage to the organisms living in thesource, as the filtering system is gentle (no powerful suction butgentle flow through the filter media), and yet in an efficient mannerthat prevents clogging.

The following drawings illustrate the system and method graphically.

FIG. 1B illustrates schematically the local backwashing apparatus 110and FIG. 2 is a schematic block diagram illustrating an integratedintake and pretreatment unit 100 for a water treatment plant 60.

Referring to FIG. 2, integrated intake and pretreatment unit 100comprises a filtering system 99 with a local backwashing apparatus 110configured to supply water to water treatment plant 60 from u watersource 70. For example, water treatment plant 60 may be a desalinationplant and water source 70 may be the sea, or water treatment plant 60may be an osmotic power production plant, receiving seawater via aseawater integrated intake and pretreatment unit 100 and river water viaa river integrated intake and pretreatment unit 100, with water source70 being the sea (or the ocean) and a river, respectively. Watertreatment plant 60 may be any other type of facility, for example,drinking ware facilities, irrigation facilities or any other system thatremoves water front a natural body of water. Water treatment plant 60operates with water received from integrated intake and pretreatmentunit 100 without any further need for pretreatment.

One drawback of the above type of local backwashing is obtainingsufficient penetration of the filter media by the enclosure to createthe required suction followed by the necessary movement of the filterbed within the enclosure. Embodiments of the present invention provide anumber of improvements over the process and apparatus of the prior artto enhance the efficiency of the local backwashing process.

Local backwashing apparatus 110 for filtering system 99 comprises (FIG.2) an enclosure 119 for carrying out the local backwashing (see FIGS.3A-3E), a supporting structure 105 movably supporting enclosure 119, thesupporting structure 105 (see FIGS. 4A-4C) configured to positionenclosure 119 at a specified spot on the surface, a pneumatic system 140in fluid communication with an upper part of the enclosure 119 andconfigured to determine an air pressure in the upper part, a pipe system133 connecting the upper part of enclosure 119 with pneumatic system 140and with a discharge structure 132 for receiving wastewater with sludgegenerated in the local backwashing process, and a control unit 150connected to supporting structure 105 and pneumatic system 140 andconfigured to conduct local backwashing of consecutive partial volumesof filter media 92.

As illustrated in FIG. 1B, system 100 and method 200 backwash portionsof filter media 92 locally, using much smaller quantities of water. As aconsequence, the high level H of water 91 above filter media 92 is notnecessary and can be replaced by a much lower level h of water 91 abovefilter media 92, a fact which significantly simplifies the constructionof filter 90. For example, prior art fitters are built to allow H=3meters of water 91 above a 1.5 meter filter media layer 92, while theproposed filter may operate using less than a h=1 meter water layer. Asthe water level is reduced, pumps 143 are added so move the filteredwater through drainage layer 96 to their destination.

Using smaller amounts of backwash water also allows using filtered waterinstead of water from an external source, and most significantly backwash portions of filter media 92 during the actual filtering process,without interruption to the global process. Using smaller amounts ofbackwash water also does not require building an external reservoir forreceiving the backwash water with sludge for treatment. In principal,discharge channel 132 may be sufficient to handle the backwash water, orsludge may be separated from the water flow and treated separately by asludge treatment unit 55. Moreover, as backwashing is carried outlocally, it docs not limit the overall filter size, as globalbackwashing does. While global backwashing filters are limited to around100 m2, the proposed filtering system 99 may be built to much largersizes, for example 500-600 m2.

The actual local backwashing is carried out within a limited portion offilter media 92, e.g. enclosed in enclosure 119 that is expanded torelease sludge flora the filter media 92. Water with the sludge in isthen moved via pipe system 133 to discharge structure 132. The flow ofwater with sludge may be initiated pneumatically by pneumatic system 140over a three way valve 135 that prevents the water flow from reaching anair pump (not shown) of pneumatic system 140. The pipe system 133comprises valves 134 for regulating air and water flow therethrough, asexplained below.

FIGS. 3A-3E schematically illustrate the operation of local backwashingapparatus 110 within a filtering system, according to some embodimentsof the invention. Local backwashing apparatus 110 for filtering system99 comprises (FIG. 2) an enclosure 119 having an open lower end andpositioned above a surface of filter media of the filtering system, thefilter media 92 being supported by a drainage layer.

Enclosure 119 generally comprises an inverted “U” or bell-shapedenclosure having continuous side walls 109 and a roof 111. The base ofthe side walls converge together to form sharp edges 113 therebyproviding a mouth to the enclosure of a smaller cross-section “X” thanthe cross-section “Y” of the main body of the enclosure. Enclosure 119may have two main positions—an inactive position 117 and an insertedposition 118. In the inactive position 117, an open lower end 128 ofenclosure 119 is plunged in water 91 above filter media 92, e.g. onsupporting structure 105 such as a bridge or a crane. In insertedposition 118, open lower end 128 of enclosure 119 is inserted intofilter media 92, enclosing a portion of filter media 92 for backwashing.The sharp edges 113 assist in inserting the enclosure into the filtermedia and moreover, movement of sand into the enclosure is encourageddue to the larger volume of the main body of the enclosure compared tothe smaller area of the mouth. In contrast, with prior art enclosuresthat have diverging or straight sides provide greater resistance tomovement of the sand into the enclosure.

In inserted position 118 enclosure 119 is supported upon drainage layer96 and isolates the portion of filter media 92 from the surroundingfilter media 92. Enclosure 119 is arranged to backwash this portionduring the continuing filtration of water 91 in filter 90, as explainedbelow. Pneumatic system 140 is connected to an upper closed end 127 ofenclosure 119 and is arranged to determine a pressure in upper closedend 127.

Pneumatic system 140 is connected to upper end 127 and dischargestructure 132 via valves 134, 135 that regulate air and water flow toand from enclosure 119. Once water flow is established (priming), itcontinues due to the hydrostatic pressure difference that results fromthe difference in water level h between enclosure 119 and dischargestructure 132. The regulation of air and water flow is earned out bycontrolling valves 134, 135 controlled by controlling unit 150.Pneumatic system 140 is further arranged to interrupt the water flow andincrease air pressure in upper end 127.

Control system 150 conducts local backwashing of consecutive partialvolumes of filter media 92 by the following stages. These stages arealso illustrated in FIG. 5, being a schematic flowchart illustratingmethod 200 of supplying water treatment plant 60 with water andbackwashing of filtering system 99, according to some embodiments of theinvention.

First, enclosure 119 is positioned at a specified spot on the surfacethat corresponds to the partial volume of filter media, i.e. over thespot that is to be backwashed (stage 225). The positioning may becarried out by lifting enclosure 119 above the surface and then loweringit into the filter media, by dragging or rolling enclosure 119 on thesurface, or by any other positioning method. Then (FIG. 3A), enclosure119 is sunk into filter media 92 (stage 230) until enclosure 119 issupported on drainage layer 96 (FIG. 3B). A water inlet and valve 120 isprovided near to the base of the enclosure which is opened during thepositioning of the enclosure onto the filter media 92. This assists inembedding the end of the side walls of the enclosure within the filtermedia. In this respect, the filter media is highly compacted andtherefore difficult to cut-through by the walls of the enclosure. Thedelivery of water to the sand reduces the stickiness of the sand,creating turbulence and encouraging the sand to start flowing up intothe enclosure. As this occurs, a vacuum pump is switched on to reducethe air pressure in the upper part 127 of enclosure 119 (stage 232)through pneumatic system 140 once open lower end 128 of enclosure 119 isimmersed in filter media 92 (129E in FIG. 3E, representing the end of aformer local backwashing process), to enclose the partial volume offilter media 92 within enclosure 119 (stage 234). The water inlet isthen gradually closed so water is no longer delivered to the sand. Atthe beginning of the sinking process, lower end 128 is in the filtermedia and partially filled wish water 129A, at the end of the sinkingprocess, lower end 128 is filled with a local portion of the filteringmedia 129B. To initiate sinking stage 230, it is favorable that edge 109is within filter media 92, to prevent excessive water flow that mayinterfere with the process.

Local backwashing of the partial volume of filter media 92 enclosed inenclosure 119 is then generated during continued operation of globalfiltering in the filtering system (through filter media outside theenclosure in the filtering system) (stage 240), by generating suctionthrough pneumatic system 140 (stage 242) that initiates a water flowfrom upper part 127 of enclosure 119 through pipe system 133 todischarge structure 132 (stage 250).

The water flow introduces into the enclosed partial volume of filtermedia filtered water from drainage layer 96 that is filtered by the restof the filter media, surrounding enclosure 119 (stage 244) which expandsthe enclosed filter media and releases sludge therefrom (stage 246) tothe water flow that flows to discharge structure 132 (stage 250). Waterflow is maintained by utilizing the height difference h between thewater level in enclosure 119 (that may locally be higher than the waterlevel in filter 90) (stage 252). An edge 109 (FIG. 3A) of open lower end128 of enclosure 119 may be shaped to prevent filter media flow intoenclosed partial volume 129C (FIG. 3C). As side walls 109 are supportedon an upper layer 96A of drainage layer 96 (upper layer 96A of drainagelayer 96 supports filter media 92 and allows water move through, a lowerlayer 96B collects the water), good contact may be achieved.Furthermore, the form of edge 109 may be designed to transmit forces(weight and contacting impact) from enclosure 119 to upper layer 96A ina non-damaging manner. Local backwashing is carried out by water fromdrainage layer 96 moving into the enclosed filter media, expanding itand removing sludge from the filter media particles. Hence, filteredwater that is filtered during the local backwashing by other parts ofthe filter media outside the enclosure, is used for backwashing theenclosed filter media, without need for an external water source.

Expanded filter media 129C fills most of the volume of enclosure 119,and is agitated due to the suction, water flow into the enclosure andwater flow out of the enclosure 119. The agitation separates the sludgeparticles gravitationally from the filter media, as sludge particlesfloat in the water and filter media sinks. The portion of backwashedfilter media may be allowed to settle before enclosure 159 is removed,in order to prevent horizontal mixing of filter media 92 which maydecrease the efficiency of the local back washing.

Finally, enclosure 119 is raised above the surface of filter media 92(stage 260) to release the backwashed enclosed volume of filter media,by injecting air and increasing air pressure in the upper part ofenclosure 119 (stage 262) through the pneumatic system to floatenclosure 119 above filter media 92 (stage 264). Settled backwashedfilter media 129D starts filtering water 91 at high efficiency onceenclosure 119 is removed.

The backwashing of partial volumes may be carried out sequentially(stage 272) to backwash a whole volume of filter media 92 at a frequencybetween five times a day and once in three months, depending on thesizes of filter 90 and enclosure 119, the clogging rate of the fittermedia, water throughput, technical parameters of operation, etc.

Method 200 may further include supplying water treatment plant 60 withwater by constructing an intake unit as filtering system 99 (stage 210)with filter media 92 and applying local backwashing (stage 220) tomaintain filtering system 99 operative.

FIGS. 4A-4C schematically illustrate integrated intake and pretreatmentunits 100 for water treatment plant 60 with various configurations ofsupporting structure 105 for local backwashing apparatus 110, accordingto some embodiments of the invention.

FIG. 4A illustrates a concrete filter 90 as filtering system 99 with afixed bridge as supporting structure 105 (pipe system connectingenclosure 119 to discharge structure is not shown).

FIG. 4B illustrates a constructed filtering system 99 with a floatingbridge as supporting structure 105 (pipe system connecting enclosure 119to discharge structure is not shown). The construction may be carriedout e.g. by digging and lining a volume for filter 90 and then bringingfilter 90 into contact with water source 70.

FIG. 4C illustrates a constructed filtering system 99 with rotatingbridges as supporting structure 105 (pipe system connecting enclosure.119 to discharge structure is not shown). In the illustrated example,enclosures are mounted pairwise on the rotating bridges to achieve ahigh rate of local backwashing. Multiple enclosures 119 may be used withany configuration of supporting structure 105 and control unit 150 maybe adapted to control and manage any number of simultaneously operatingenclosures 119. In a similar manner, enclosure 119 may be supported by acrane as supporting structure 103.

In embodiments, filtering system 99 may be elongated and enclosure 119may span a width of filtering system 99, e.g. have the width of bridges105 in FIGS. 4A and 4B. In some embodiments, open lower end 128 ofenclosure 159 may be small, e.g. have an area between 0.1 m2 and 10 m2to simplify pipe system 133, pneumatic system 140, supporting structure105 and their control.

Integrated intake and pretreatment unit 100 prevents damage to thenatural fauna in the body of water from where water is taken. As theintake is carried out through the filter media, there are no open pipesor intake screens that damage organisms such as fish, and no open fastflowing wafer bodies that may remove and kill organisms.

In another embodiment of the present invention, a novel two-stepmechanism is incorporated into the method and apparatus to improve thesealing of the enclosure 119 within a subarea of a filter. In thisrespect, using only mechanical entry for the enclosure may damage theconstruction of the enclosure and/or the drainage pipes 96 due to therepetitive stress applied when the walls of the enclosure are forcedinto the filter bed. In the present invention, the enclosure is insertedusing a first mechanical step (A) and a second pressure differentialstep (B), as illustrated in FIGS. 6A and 6B.

A mechanical pusher 300, such as a piston-operated pusher, is used toinsert the enclosure the majority of the way into the fitter to beenclosed, as illustrated in FIG. 6A. For example, the mechanical pushermay insert the enclosure at least 95% into the filter media 92 but lessthan 100% into the bed. The enclosure 119 is then moved the remainingdistance B (1-10 cm, preferably around 5 cm) by a pressure differentialbetween the inside of the enclosure 119 and the outside of the enclosurewhich allows the enclosure to gradually close the small gap to the floorof the filter bed, enabling the enclosure to land softly on the floorminimizing damage to both the enclosure 119 and the drainage pipe 95. Itis to be appreciated that this two-step mechanism is preferably employedwith both converging side walls on the enclosure and the introduction ofwater into the enclosure thereby greatly enhancing the sealing of thefilter bed area within the enclosure, albeit each may be appliedseparately.

In the above description, an embodiment is an example or implementationof the invention. The various appearances of “one embodiment”, “anembodiment” or “some embodiments” do not necessarily all refer to thesame embodiment.

Although various features of the invention may be described in thecontext of a single embodiment, the features may also lie providedseparately or in any suitable combination. Conversely, although theinvention may be described herein in the context of separate embodimentsfor clarity, the invention may also be implemented in a singleembodiment.

Embodiments of the invention may include features from differentembodiments disclosed above, and embodiments may incorporate elementsfrom other embodiments disclosed above. The disclosure of elements ofthe invention in the context of a specific embodiment is not to be takenas limiting their used in the specific embodiment alone.

Furthermore, it is to be understood that the invention can be carriedout or practiced in various ways and that the invention can beimplemented in embodiments other than the ones outlined in thedescription above.

The invention is not limited to those diagrams or to the correspondingdescriptions. For example, flow need not move through each illustratedbox or state, or in exactly the same order as illustrated and described.

Meanings of technical and scientific terms used herein are to becommonly understood as by one of ordinary skill in the art to which theinvention belongs, unless otherwise defined.

While the invention has been described with respect to a limited numberof embodiments, these should not be construed as limitations on thescope of the invention, but rather as exemplifications of some of thepreferred embodiments. Other possible variations, modifications, andapplications are also within the scope of the invention, as limited bythe claims.

What is claimed is:
 1. A local backwashing apparatus for a filteringsystem comprising: an enclosure having an open lower end andpositionable above a surface of filter media of the filtering system,the filter media supported by a drainage layer, a pneumatic system influid communication with an upper part of the enclosure and configuredto determine an air pressure in an upper part, a pipe system connectingthe upper part of the enclosure with the pneumatic system and with adischarge structure, and a control unit connected to the pneumaticsystem and configured to conduct local backwashing of consecutivepartial volumes of the filter media by sinking the enclosure into thefilter media until the enclosure is supported on the drainage layer byreducing the air pressure in the upper part of the enclosure through thepneumatic system once the open lower end of the enclosure is immersed infilter media, to enclose the partial volume of filter media within theenclosure and generating local backwashing of the partial volume of thefilter media enclosed in the enclosure, during continued operation ofglobal filtering through filter media outside the enclosure in thefiltering system, by generating suction through the pneumatic systemthat initiates a water flow from the upper part of the enclosure throughthe pipe system to the discharge structure, wherein the water flowintroduces into the lower end of the enclosed partial volume of filtermedia filtered water from the drainage layer which expands the enclosedfilter media and releases sludge therefrom to the water flow that flowsto the discharge structure, and raising the enclosure above the surfaceof the filter media to release the backwashed enclosed volume of filtermedia, by injecting air and increasing air pressure in the upper part ofthe enclosure through the pneumatic system to float the enclosure abovethe filter media; characterized in that the enclosure is connected to amechanical member configured to forcibly drive the enclosure into thefilter media and release said force prior to contact of the lower end ofthe enclosure with the drainage layer, the lower end of the enclosurebeing brought into contact with the drainage layer through a pressuredifferential between the interior and exterior of the enclosure.
 2. Thelocal backwashing apparatus according to claim 1, wherein the apparatusfurther comprises a supporting structure movably supporting theenclosure, the supporting structure configured to position the enclosureat specified spots on the surface of the filter media.
 3. The localbackwashing apparatus of claim 2 wherein the supporting structure is atleast one of: a fixed bridge, a floating bridge, a rotating bridge and acrane.
 4. The local backwashing apparatus of claim 1, wherein a heightof the enclosure is configured to be larger than a height of the waterabove the filter media.
 5. An integrated intake and pre-treatment unitfor a water treatment plant comprising a filtering system with the localbackwashing apparatus of claim
 1. 6. A method of backwashing a filteringsystem having a layer of filter media supported by a drainage layer, themethod comprising sequentially backwashing partial volumes of the filtermedia by: (i) driving an enclosure into the filter media until theenclosure is above the drainage layer by mechanically forcing theenclosure through the media; (ii) reducing, air pressure in an upperpart of the enclosure once an open lower end of the enclosure isimmersed in filter media, to enclose the partial volume of filter mediawithin the enclosure; (iii) allowing the enclosure to come into contactwith the drainage layer by a pressure differential between an interiorand exterior of the enclosure; (iv) generating local backwashing of thepartial volume of the filter media enclosed in the enclosure, duringcontinued operation of global filtering through filter media outside theenclosure in the filtering system, by generating suction in the upperpart of the enclosure that initiates a water flow from the upper part ofthe enclosure through a pipe system to a discharge structure, whereinthe water flow introduces into the lower end of the enclosed partialvolume of filter media filtered water from the drainage layer whichexpands the enclosed filter media and releases sludge therefrom to thewater flow; and (v) raising the enclosure above the surface of thefilter media to release the backwashed enclosed volume of filter media,by injecting air and increasing air pressure in the upper part of theenclosure to float the enclosure above the filter media.